Mixture of 1-Propanol + Ethanol

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)
5. Vapor or sublimation pressure, kPa (2)

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	323.15	0.0000
0.0000	348.15	0.0000
0.1243	323.15	0.2586
0.1305	348.15	0.2465
0.2024	323.15	0.3788
0.2059	348.15	0.3586
0.2646	323.15	0.4655
0.2750	348.15	0.4468
0.3802	323.15	0.5937
0.3890	348.15	0.5745
0.4524	323.15	0.6645
0.4573	348.15	0.6396
0.5374	323.15	0.7354
0.5430	348.15	0.7174
0.7505	323.15	0.8763
0.7542	348.15	0.8647
0.8453	323.15	0.9272
0.8466	348.15	0.9199
0.8584	348.15	0.9253
0.8956	348.15	0.9462
0.9236	348.15	0.9604
0.9613	348.15	0.9803
0.9848	323.15	0.9927
1.0000	323.15	1.0000
1.0000	348.15	1.0000

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
403.20	0.0011	0.0019
403.20	0.0426	0.0754
403.20	0.2914	0.4042
403.20	0.4290	0.5744
403.20	0.6919	0.7974
403.20	0.9983	0.9993
413.20	0.0007	0.0022
413.20	0.0513	0.0747
413.20	0.2541	0.3642
413.20	0.4563	0.5959
413.20	0.7001	0.8014
413.20	0.9998	0.9995
423.20	0.0007	0.0026
423.20	0.0496	0.0714
423.20	0.2617	0.3608
423.20	0.4553	0.5846
423.20	0.6916	0.7879
423.20	0.9983	0.9993

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (2) - Gas
0.0000	323.15	0.0000
0.0000	348.15	0.0000
0.1243	323.15	0.2586
0.1305	348.15	0.2465
0.2024	323.15	0.3788
0.2059	348.15	0.3586
0.2646	323.15	0.4655
0.2750	348.15	0.4468
0.3802	323.15	0.5937
0.3890	348.15	0.5745
0.4524	323.15	0.6645
0.4573	348.15	0.6396
0.5374	323.15	0.7354
0.5430	348.15	0.7174
0.7505	323.15	0.8763
0.7542	348.15	0.8647
0.8453	323.15	0.9272
0.8466	348.15	0.9199
0.8584	348.15	0.9253
0.8956	348.15	0.9462
0.9236	348.15	0.9604
0.9613	348.15	0.9803
0.9848	323.15	0.9927
1.0000	323.15	1.0000
1.0000	348.15	1.0000

Mole fraction of Ethanol (2) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
403.20	0.0011	0.0019
403.20	0.0426	0.0754
403.20	0.2914	0.4042
403.20	0.4290	0.5744
403.20	0.6919	0.7974
403.20	0.9983	0.9993
413.20	0.0007	0.0022
413.20	0.0513	0.0747
413.20	0.2541	0.3642
413.20	0.4563	0.5959
413.20	0.7001	0.8014
413.20	0.9998	0.9995
423.20	0.0007	0.0026
423.20	0.0496	0.0714
423.20	0.2617	0.3608
423.20	0.4553	0.5846
423.20	0.6916	0.7879
423.20	0.9983	0.9993

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0022
293.15	0.1000	0.0020
293.15	0.2000	0.0019
293.15	0.3010	0.0018
293.15	0.4000	0.0017
293.15	0.5000	0.0016
293.15	0.5990	0.0015
293.15	0.7010	0.0014
293.15	0.8000	0.0013
293.15	0.9000	0.0012
293.15	1.0000	0.0012
298.15	0.0000	0.0019
298.15	0.1000	0.0018
298.15	0.2000	0.0017
298.15	0.3010	0.0016
298.15	0.4000	0.0015
298.15	0.5000	0.0014
298.15	0.5990	0.0014
298.15	0.7010	0.0013
298.15	0.8000	0.0012
298.15	0.9000	0.0011
298.15	1.0000	0.0011
303.15	0.0000	0.0017
303.15	0.1000	0.0016
303.15	0.2000	0.0015
303.15	0.3010	0.0015
303.15	0.4000	0.0014
303.15	0.5000	0.0013
303.15	0.5990	0.0012
303.15	0.7010	0.0012
303.15	0.8000	0.0011
303.15	0.9000	0.0010
303.15	1.0000	0.0010
308.15	0.0000	0.0015
308.15	0.1000	0.0014
308.15	0.2000	0.0014
308.15	0.3010	0.0013
308.15	0.4000	0.0012
308.15	0.5000	0.0012
308.15	0.5990	0.0011
308.15	0.7010	0.0010
308.15	0.8000	0.0010
308.15	0.9000	0.0009
308.15	1.0000	0.0009
313.15	0.0000	0.0014
313.15	0.1000	0.0013
313.15	0.2000	0.0012
313.15	0.3010	0.0012
313.15	0.4000	0.0011
313.15	0.5000	0.0011
313.15	0.5990	0.0010
313.15	0.7010	0.0010
313.15	0.8000	0.0009
313.15	0.9000	0.0009
313.15	1.0000	0.0008
318.15	0.0000	0.0012
318.15	0.1000	0.0012
318.15	0.2000	0.0011
318.15	0.3010	0.0011
318.15	0.4000	0.0010
318.15	0.5000	0.0010
318.15	0.5990	0.0009
318.15	0.7010	0.0009
318.15	0.8000	0.0008
318.15	0.9000	0.0008
318.15	1.0000	0.0008
323.15	0.0000	0.0011
323.15	0.1000	0.0011
323.15	0.2000	0.0010
323.15	0.3010	0.0010
323.15	0.4000	0.0009
323.15	0.5000	0.0009
323.15	0.5990	0.0008
323.15	0.7010	0.0008
323.15	0.8000	0.0008
323.15	0.9000	0.0007
323.15	1.0000	0.0007
328.15	0.0000	0.0010
328.15	0.1000	0.0010
328.15	0.2000	0.0009
328.15	0.3010	0.0009
328.15	0.4000	0.0008
328.15	0.5000	0.0008
328.15	0.5990	0.0008
328.15	0.7010	0.0007
328.15	0.8000	0.0007
328.15	0.9000	0.0007
328.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0022
293.15	0.1000	0.0020
293.15	0.2000	0.0019
293.15	0.3010	0.0018
293.15	0.4000	0.0017
293.15	0.5000	0.0016
293.15	0.5990	0.0015
293.15	0.7010	0.0014
293.15	0.8000	0.0013
293.15	0.9000	0.0012
293.15	1.0000	0.0012
298.15	0.0000	0.0019
298.15	0.1000	0.0018
298.15	0.2000	0.0017
298.15	0.3010	0.0016
298.15	0.4000	0.0015
298.15	0.5000	0.0014
298.15	0.5990	0.0014
298.15	0.7010	0.0013
298.15	0.8000	0.0012
298.15	0.9000	0.0011
298.15	1.0000	0.0011
303.15	0.0000	0.0017
303.15	0.1000	0.0016
303.15	0.2000	0.0015
303.15	0.3010	0.0015
303.15	0.4000	0.0014
303.15	0.5000	0.0013
303.15	0.5990	0.0012
303.15	0.7010	0.0012
303.15	0.8000	0.0011
303.15	0.9000	0.0010
303.15	1.0000	0.0010
308.15	0.0000	0.0015
308.15	0.1000	0.0014
308.15	0.2000	0.0014
308.15	0.3010	0.0013
308.15	0.4000	0.0012
308.15	0.5000	0.0012
308.15	0.5990	0.0011
308.15	0.7010	0.0010
308.15	0.8000	0.0010
308.15	0.9000	0.0009
308.15	1.0000	0.0009
313.15	0.0000	0.0014
313.15	0.1000	0.0013
313.15	0.2000	0.0012
313.15	0.3010	0.0012
313.15	0.4000	0.0011
313.15	0.5000	0.0011
313.15	0.5990	0.0010
313.15	0.7010	0.0010
313.15	0.8000	0.0009
313.15	0.9000	0.0009
313.15	1.0000	0.0008
318.15	0.0000	0.0012
318.15	0.1000	0.0012
318.15	0.2000	0.0011
318.15	0.3010	0.0011
318.15	0.4000	0.0010
318.15	0.5000	0.0010
318.15	0.5990	0.0009
318.15	0.7010	0.0009
318.15	0.8000	0.0008
318.15	0.9000	0.0008
318.15	1.0000	0.0008
323.15	0.0000	0.0011
323.15	0.1000	0.0011
323.15	0.2000	0.0010
323.15	0.3010	0.0010
323.15	0.4000	0.0009
323.15	0.5000	0.0009
323.15	0.5990	0.0008
323.15	0.7010	0.0008
323.15	0.8000	0.0008
323.15	0.9000	0.0007
323.15	1.0000	0.0007
328.15	0.0000	0.0010
328.15	0.1000	0.0010
328.15	0.2000	0.0009
328.15	0.3010	0.0009
328.15	0.4000	0.0008
328.15	0.5000	0.0008
328.15	0.5990	0.0008
328.15	0.7010	0.0007
328.15	0.8000	0.0007
328.15	0.9000	0.0007
328.15	1.0000	0.0006

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	323.15	12.17
0.0000	348.15	40.95
0.1243	323.15	14.38
0.1305	348.15	47.30
0.2024	323.15	15.71
0.2059	348.15	50.94
0.2646	323.15	16.84
0.2750	348.15	54.19
0.3802	323.15	18.80
0.3890	348.15	59.66
0.4524	323.15	20.08
0.4573	348.15	62.99
0.5374	323.15	21.56
0.5430	348.15	67.13
0.7505	323.15	25.24
0.7542	348.15	77.25
0.8453	323.15	26.85
0.8466	348.15	81.60
0.8584	348.15	82.22
0.8956	348.15	83.90
0.9236	348.15	85.29
0.9613	348.15	87.08
0.9848	323.15	29.25
1.0000	323.15	29.48
1.0000	348.15	88.84

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	323.15	12.17
0.0000	348.15	40.95
0.1243	323.15	14.38
0.1305	348.15	47.30
0.2024	323.15	15.71
0.2059	348.15	50.94
0.2646	323.15	16.84
0.2750	348.15	54.19
0.3802	323.15	18.80
0.3890	348.15	59.66
0.4524	323.15	20.08
0.4573	348.15	62.99
0.5374	323.15	21.56
0.5430	348.15	67.13
0.7505	323.15	25.24
0.7542	348.15	77.25
0.8453	323.15	26.85
0.8466	348.15	81.60
0.8584	348.15	82.22
0.8956	348.15	83.90
0.9236	348.15	85.29
0.9613	348.15	87.08
0.9848	323.15	29.25
1.0000	323.15	29.48
1.0000	348.15	88.84

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	803.58
293.15	0.1000	802.08
293.15	0.2000	800.86
293.15	0.3010	799.68
293.15	0.4000	798.4
293.15	0.5000	797.31
293.15	0.5990	795.87
293.15	0.7010	794.36
293.15	0.8000	792.88
293.15	0.9000	791.44
293.15	1.0000	790.13
298.15	0.0000	799.59
298.15	0.1000	798.08
298.15	0.2000	796.82
298.15	0.3010	795.65
298.15	0.4000	794.33
298.15	0.5000	793.22
298.15	0.5990	791.75
298.15	0.7010	790.21
298.15	0.8000	788.69
298.15	0.9000	787.22
298.15	1.0000	785.86
303.15	0.0000	795.58
303.15	0.1000	794.05
303.15	0.2000	792.77
303.15	0.3010	791.57
303.15	0.4000	790.22
303.15	0.5000	789.08
303.15	0.5990	787.59
303.15	0.7010	786.02
303.15	0.8000	784.47
303.15	0.9000	782.96
303.15	1.0000	781.56
308.15	0.0000	791.53
308.15	0.1000	789.98
308.15	0.2000	788.8
308.15	0.3010	787.45
308.15	0.4000	786.08
308.15	0.5000	784.92
308.15	0.5990	783.4
308.15	0.7010	781.8
308.15	0.8000	780.21
308.15	0.9000	778.67
308.15	1.0000	777.23
313.15	0.0000	787.44
313.15	0.1000	785.86
313.15	0.2000	784.66
313.15	0.3010	783.29
313.15	0.4000	781.9
313.15	0.5000	780.71
313.15	0.5990	779.16
313.15	0.7010	777.53
313.15	0.8000	775.91
313.15	0.9000	774.33
313.15	1.0000	772.86
318.15	0.0000	783.3
318.15	0.1000	781.7
318.15	0.2000	780.48
318.15	0.3010	779.09
318.15	0.4000	777.68
318.15	0.5000	776.45
318.15	0.5990	774.88
318.15	0.7010	773.22
318.15	0.8000	771.56
318.15	0.9000	769.95
318.15	1.0000	768.44
323.15	0.0000	779.11
323.15	0.1000	777.49
323.15	0.2000	776.24
323.15	0.3010	774.83
323.15	0.4000	773.39
323.15	0.5000	772.14
323.15	0.5990	770.54
323.15	0.7010	768.85
323.15	0.8000	767.16
323.15	0.9000	765.52
323.15	1.0000	763.97
328.15	0.0000	774.86
328.15	0.1000	773.22
328.15	0.2000	771.95
328.15	0.3010	770.52
328.15	0.4000	769.06
328.15	0.5000	767.78
328.15	0.5990	766.15
328.15	0.7010	764.43
328.15	0.8000	762.71
328.15	0.9000	761.02
328.15	1.0000	759.44

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	803.58
293.15	0.1000	802.08
293.15	0.2000	800.86
293.15	0.3010	799.68
293.15	0.4000	798.4
293.15	0.5000	797.31
293.15	0.5990	795.87
293.15	0.7010	794.36
293.15	0.8000	792.88
293.15	0.9000	791.44
293.15	1.0000	790.13
298.15	0.0000	799.59
298.15	0.1000	798.08
298.15	0.2000	796.82
298.15	0.3010	795.65
298.15	0.4000	794.33
298.15	0.5000	793.22
298.15	0.5990	791.75
298.15	0.7010	790.21
298.15	0.8000	788.69
298.15	0.9000	787.22
298.15	1.0000	785.86
303.15	0.0000	795.58
303.15	0.1000	794.05
303.15	0.2000	792.77
303.15	0.3010	791.57
303.15	0.4000	790.22
303.15	0.5000	789.08
303.15	0.5990	787.59
303.15	0.7010	786.02
303.15	0.8000	784.47
303.15	0.9000	782.96
303.15	1.0000	781.56
308.15	0.0000	791.53
308.15	0.1000	789.98
308.15	0.2000	788.8
308.15	0.3010	787.45
308.15	0.4000	786.08
308.15	0.5000	784.92
308.15	0.5990	783.4
308.15	0.7010	781.8
308.15	0.8000	780.21
308.15	0.9000	778.67
308.15	1.0000	777.23
313.15	0.0000	787.44
313.15	0.1000	785.86
313.15	0.2000	784.66
313.15	0.3010	783.29
313.15	0.4000	781.9
313.15	0.5000	780.71
313.15	0.5990	779.16
313.15	0.7010	777.53
313.15	0.8000	775.91
313.15	0.9000	774.33
313.15	1.0000	772.86
318.15	0.0000	783.3
318.15	0.1000	781.7
318.15	0.2000	780.48
318.15	0.3010	779.09
318.15	0.4000	777.68
318.15	0.5000	776.45
318.15	0.5990	774.88
318.15	0.7010	773.22
318.15	0.8000	771.56
318.15	0.9000	769.95
318.15	1.0000	768.44
323.15	0.0000	779.11
323.15	0.1000	777.49
323.15	0.2000	776.24
323.15	0.3010	774.83
323.15	0.4000	773.39
323.15	0.5000	772.14
323.15	0.5990	770.54
323.15	0.7010	768.85
323.15	0.8000	767.16
323.15	0.9000	765.52
323.15	1.0000	763.97
328.15	0.0000	774.86
328.15	0.1000	773.22
328.15	0.2000	771.95
328.15	0.3010	770.52
328.15	0.4000	769.06
328.15	0.5000	767.78
328.15	0.5990	766.15
328.15	0.7010	764.43
328.15	0.8000	762.71
328.15	0.9000	761.02
328.15	1.0000	759.44

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
403.20	0.0011	304.20
403.20	0.0426	319.80
403.20	0.2914	384.60
403.20	0.4290	416.60
403.20	0.6919	487.40
403.20	0.9983	557.60
413.20	0.0007	408.00
413.20	0.0513	429.00
413.20	0.2541	493.90
413.20	0.4563	564.10
413.20	0.7001	640.40
413.20	0.9998	736.30
423.20	0.0007	546.10
423.20	0.0496	565.30
423.20	0.2617	648.30
423.20	0.4553	725.30
423.20	0.6916	822.00
423.20	0.9983	967.40

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Vapor or sublimation pressure, kPa - Gas
403.20	0.0011	304.20
403.20	0.0426	319.80
403.20	0.2914	384.60
403.20	0.4290	416.60
403.20	0.6919	487.40
403.20	0.9983	557.60
413.20	0.0007	408.00
413.20	0.0513	429.00
413.20	0.2541	493.90
413.20	0.4563	564.10
413.20	0.7001	640.40
413.20	0.9998	736.30
423.20	0.0007	546.10
423.20	0.0496	565.30
423.20	0.2617	648.30
423.20	0.4553	725.30
423.20	0.6916	822.00
423.20	0.9983	967.40

Sources

• Vapour-liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction
• High-temperature vapor-liquid equilibrium for ethanol-1-propanol mixtures and modeling with SAFT-VR
• Densities and Viscosities for Binary Liquid Mixtures of Ethanol + 1-Propanol, 1-Butanol, and 1-Pentanol from (293.15 to 328.15) K at 0.1 MPa